US2014291207A1PendingUtilityA1

Method for producing a diesel fuel

Assignee: TELYASHEV RAUSHAN GUMEROVICHPriority: Jun 22, 2011Filed: Jun 19, 2012Published: Oct 2, 2014
Est. expiryJun 22, 2031(~4.9 yrs left)· nominal 20-yr term from priority
C10G 67/14C10G 45/08C10G 7/00C10G 21/27C10G 2300/301C10G 2300/1051C10G 2300/202C10L 1/08C10G 2300/1055C10G 21/16C10G 67/04C10G 21/20C10G 2400/04C10G 31/08
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Claims

Abstract

A method relating to oil refining, which can be used to produce low-sulfur diesel fuel, comprising oil demineralization and distillation, and extraction and mixing of diesel fractions, followed by hydrogen refining of the mixture. In an atmospheric tower, two diesel fractions that boil at 171-341° C. and 199-360° C. are extracted. The 199-360° C. fraction is sent for liquid extraction to purify it from benzalkylthiophens. Amide, a product of organic amine interaction with organic acid, is used as the extractant. Fractions are then mixed, maintaining the balance ratio (based on the output) of 171-341° C. and 199-360 ° C. after refining. When refined using the ASTM D-86 method, the mixture of these fractions has an end boiling point no higher than 360° C. The technical result is production of diesel fuel with a 171-360° C. fractional composition and sulfur content of no higher than 10 ppm.

Claims

exact text as granted — not AI-modified
What is claimed: 
     
         1 . A method for production of diesel fuel comprising oil demineralization and distillation, extraction and mixing of diesel fractions followed by hydrogen refining of a mixture, wherein,
 during distillation in an atmospheric tower, two diesel fractions boiling at 171-341° C. and 199-360° C. are extracted,   the 199-360° C. fraction is sent for liquid extraction to purify said 199-360° C. fraction from benzalkylthiophens using amide as an extractant, a product of organic amine interaction with organic acid, and   the 171-341° C. and 199-360° C. fractions are mixed after refining, and wherein a mixture of these fractions, when refined using an ASTM D-86 method, has an end boiling point no higher than 360° C.   
     
     
         2 . The method of  claim 1 , wherein the produced mixture is subject to hydrogen refining on an aluminum-cobalt-molybdenum or aluminum-nickel-molybdenum catalyst.

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